Method for operating a firing plant

ABSTRACT

A method for operating a firing plant with at least one combustion chamber and with at least one burner for producing hot gas, especially a gas turbine, preferably of a power generating plant, includes an operating characteristic for operating the combustion chamber close to the lean extinction limit defined in the form of a burner group staging ratio (BGV Rich ). The pressure pulsations (Puls Actual ) which are measured in the combustion chamber are processed by a filter device ( 2 ) and converted into corresponding signals (Puls Actual,Filter (t)). An exceeding/falling short of at least one pulsation limiting value (Puls Limit ) is monitored by a monitoring device ( 3 ) and adapts a pulsation reference value (Puls Ref ) in dependence upon the monitoring. The processed pressure pulsations (Puls Actual,Filter (t)) are then compared with the adapted pulsation reference value (Puls Ref,adapt ), and, from this, a correction value ΔBGV is determined, by which the burner group staging ratio (BGV Rich ) is corrected, and as a result operation of the firing plant close to the lean extinction limit is realized.

This application is a Continuation of, and claims priority under 35 U.S.C. § 120 to, International App. No. PCT/EP2006/068662, filed 20 Nov. 2006, and claims priority therethrough under 35 U.S.C. §§ 119, 365 to Swiss App. No. 00049/06, filed 11 Jan. 2006, the entireties of which are incorporated by reference herein.

BACKGROUND

1. Field of Endeavor

The present invention relates to a method for operating a firing plant with at least one combustion chamber and with at least one burner for producing hot gas, especially a gas turbine, preferably in a power generating plant. The invention also relates to a firing plant with at least one combustion chamber and at least one burner for producing hot gas.

2. Brief Description of the Related Art

A firing plant, for example a gas turbine, customarily has at least one combustion chamber with at least one burner. Furthermore, a fuel supply system is always provided, by which the burners are supplied with fuel. With regard to regulations which are becoming ever stricter concerning limiting values which are to be observed for pollutant emissions, it is sought to operate the burners as close as possible to the lean extinction limit. As a result of such a lean operation, especially the creation of harmful NO_(x) emissions can be reduced.

The influencing parameters which determine the extinction limit vary in this case during operation of a gas turbine. Such influencing parameters, for example, are boundary conditions such as the ambient temperature, the relative air humidity, the air mass flow which depends especially upon the operating state of the upstream compressor, and the composition of the fuel which is currently used, etc. The burners, with regard to their fuel feed, are frequently divided into two or more groups so that an influence can be exerted upon the equivalence ratio of the combustion process. In this case, the fuel feed to the two or more burner groups is customarily controlled in dependence upon the aforementioned factors. Since, however, not all important parameters, and especially not all changes to each time point, can be adequately taken into consideration, a predefined fuel staging ratio or burner group staging ratio is always selected with a certain safety margin to the lean extinction limit.

This safety margin is to ensure that even during a change of the individual boundary conditions, which act differently upon the stability of the combustion process, a stable operation of the individual burners is ensured. A stable operating state takes highest priority, especially in the case of power generating plants which are used for electric power generation, so that the safety margin is greater than is absolutely necessary and consequently higher NO_(x) emissions are accepted.

SUMMARY

The present invention starts at this point. One of numerous aspect of the present invention deals with an operating method of the aforementioned type, which especially enables stable operation of the combustion chamber which is as close as possible to the lean extinction point.

Another aspect of the present invention includes controlling the fuel feed to the burners of the combustion chamber in dependence upon pressure pulsations which occur in the combustion chamber, wherein the controlling is achieved by a comparison of the pressure pulsations which occur and are conditioned in the combustion chamber with predetermined and adapted pulsation reference values. One exemplary embodiment uses the knowledge that the pressure pulsations increase as the combustion process approaches the lean extinction limit. First of all, therefore, an operating characteristic for operating the combustion chamber close to the lean extinction limit is defined or determined in the form of a burner group staging ratio, and at the same time the pressure pulsations which occur in the combustion chamber are measured and then processed by a filter device. Furthermore, a pulsation reference value, which is defined in dependence upon load, and also at least one pulsation limiting value, are defined. A monitoring device monitors pulsation exceeding/falling short of the pulsation limiting value, or the pulsation limiting values, in the process and adapts the pulsation reference value in dependence upon this monitoring. The pressure pulsations which are measured and processed in the combustion chamber are then compared with the adapted pulsation reference value and, as a result, a correction value is determined by which the operating characteristic which was defined at the beginning, i.e., the fuel feed, is corrected.

The filter device in this case has the task of reducing noise of the recorded pressure pulsation signal, as a result of which the signal quality can be significantly increased. Such improved signal quality has a positive effect upon the active control process of the operating method according to the invention. In this case the filter device can especially be designed so that it amplifies relevant signal contents, whereas it attenuates or eliminates disturbing signal contents. The increasing of the signal quality in this case can be achieved by use of an amplification factor K_(Filter) and also of a time constant T_(Filter).

The method according to an embodiment exemplifying principles of the invention has a closed-loop control circuit in which the pulsation reference value is dynamically adapted. By the method, therefore, the combustion chamber can be operated safely and yet very close to the lean extinction limit, as a result of which the NO_(x) emissions can be significantly lowered. In this case, a method according to the invention can fall back on the fact that a modern combustion chamber is always equipped with a sensor system for monitoring the pressure pulsations so that this sensor system can be utilized and consequently no additional costs ensue for instrumentation or realizing a method according to the invention with regard to recording the pressure pulsations.

According to an especially advantageous exemplary embodiment, a load-dependent pulsation reference value is established which is decreased or increased by a predetermined quantity provided that, within a defined time period, a determined number of measured pressure pulsation values lie above/below the at least one predetermined pressure pulsation limiting value. If, therefore, a determined number of pulsation values above the established pulsation limiting value occur within a predefined time period, then the pulsation reference value is decreased by a predefined quantity. The adapted pulsation reference values are used in this case for a predefined time period until a renewed adaptation of the pulsation reference value is carried out.

Further features and advantages of operating methods according to the invention result from the drawings and from the associated figure description with reference to the drawings.

BRIEF DESCRIPTION OF THE DRAWINGS

Preferred exemplary embodiments of the invention are represented in the drawings and are explained in more detail in the following description, wherein like designations refer to the same or similar, or functionally the same, components.

In the drawing, schematically in each case,

FIG. 1 shows a much schematized view of a possible sequence of the operating method according to the invention; and

FIG. 2 shows a diagram, in which the pattern of pressure pulsations is plotted.

DETAILED DESCRIPTION OF EXEMPLARY EMBODIMENTS

According to FIG. 1, a firing plant, which is not otherwise shown, with at least one combustion chamber, which is also not shown, and at least one burner for producing hot gas, has a measuring device 1 for measuring pressure pulsations Puls_(Actual)(t) which converts the pressure pulsations into preferably electrical signals and transmits the signals to a filter device 2. The filter device 2 in this case processes the signals which correspond to the measured pressure pulsations Puls_(Actual)(t), wherein preferably relevant signal components are amplified and irrelevant signal components, such as noise, are at least reduced. The filter device 2 can have a filter of the first order for processing the aforementioned signals, which amplifies the signals coming in from the measuring device 1 with an amplification factor K_(Filter). A time constant T_(Filter) can also be established in the processing of the signal, which provides the pressure pulsation signals Puls_(Actual)(t) coming in from the measuring device 1 with a time component. In order to be able to take into consideration load changes of the firing plant, it is intended to define two different amplification factors K_(Filter), specifically one for constant load cases and another for transient load cases. The pressure pulsation signals Puls_(Actual,Filter)(t), which are processed by the filter device 2, are transmitted to an evaluating/control unit 4 and in this, or by this, are compared together with an adapted pulsation reference value Puls_(Ref,adapt).

The adapted pulsation reference value Puls_(Ref,adapt) in this case is dependent upon load and is to bring about the firing plant being able to be operated as lean as possible, as a result of which a discharge of NO_(x) emissions can be reduced. Determination of the adapted pulsation reference value Puls_(Ref,adapt) in this case is carried out as follows:

First of all, a pulsation reference value Puls_(Ref) is defined or established in dependence upon the relative load. The predefined pulsation reference value Puls_(Ref) is now monitored by a monitoring device 3 and at the same time a corrected pulsation reference value Puls_(Ref,adapt) is determined in dependence upon the monitoring by the monitoring device 3. The adaptation of the pulsation reference value Puls_(Ref) in this case is carried out by the monitoring device 3 comparing the measured and preferably filtered pressure pulsations Puls_(Actual)(t) or Puls_(Actual,Filter)(t) with the predefined pulsation reference value Puls_(Ref), and in the case of exceeding or falling short of at least one pulsation limiting value Puls_(Limit), correspondingly increases or decreases, and consequently adapts, the pulsation reference value Puls_(Ref). For correction or adaptation of the established pulsation reference value Puls_(Ref), within a defined time period, a determined number of pressure pulsation values Puls_(Actual)(t) must lie above or below the at least predetermined pulsation limiting value Puls_(Limit) accordingly.

From the two input values, specifically the measured and filtered pressure pulsations Puls_(Actual,Filter) on the one hand and the adapted pulsation reference value Puls_(Ref,adapt) on the other hand, the evaluating/control unit 4 now determines a correction value ΔBGV by which the defined burner group staging ratio BGV_(Rich) which was defined at the beginning, i.e., the operating characteristic, is corrected. The determination of the correction value ΔBGV in this case is carried out by comparison of the measured and filtered pressure pulsations Puls_(Actual,Filter) with the adapted pulsation reference value Puls_(Ref,adapt). The evaluating/control unit 4 in this case for example can be formed as a proportional/integral controller, or as a purely proportional controller, or as a purely integral controller, and can operate with an amplification factor K_(PI) and also with a time constant T_(TI) which are also defined in dependence upon the relative load, like the established reference value Puls_(Ref). The original burner group staging ratio BGV_(Rich) is corrected by the correction value ΔBGV so that a burner group staging ratio BGV_(New), which is corrected and better adapted to the new boundary conditions, is achieved.

According to FIG. 2, the measured pressure pulsations Puls_(Actual) are plotted over time t. In this case, an upper pulsation limiting value Puls_(Limit1) and a lower pulsation limiting value Puls_(Limit2) can be established, which, in the case of exceeding or falling short of, brings about an adaptation of the pulsation reference value Puls_(Ref) by the monitoring device 3, provided that a determined number of pulsation values Puls_(Actual) or Puls_(Actual,Filter) within a defined time period lie below the pulsation limiting value Puls_(Limit2) or above the upper pulsation limiting value Puls_(Limit1). As a result, a region between Puls_(Limit1) and Puls_(Limit2) is therefore defined, in which no adaptation of the pulsation reference value Puls_(Ref) is carried out. It is also conceivable that only one pulsation limiting value Puls_(Limit) is defined, which, in the case of exceeding, and also in the case of falling short of this limiting value, brings about adaptation of the pulsation reference value Puls_(Ref). A region in which no adaptation of the pulsation reference value Puls_(Ref) is carried out is therefore not provided in the case of such an embodiment.

A further variant, in which an adaptation of the pulsation reference value Puls_(Ref) is carried out, in case within a shorter time period few pulsation values Puls_(Actual) lie above a higher pulsation limiting value, is also conceivable. For adaptation, therefore, either a certain number of pulsation values Puls_(Actual) which, within a certain time interval, exceed the upper pulsation limiting value Puls_(Limit1), are necessary, or a lower number, in comparison to it, of pulsation values Puls_(Actual) which, within a shorter time period lie above a pulsation limiting value, which is higher than the upper pulsation limiting value Puls_(Limit1), are necessary. The same can apply in a corresponding way to the lower pulsation limiting value Puls_(Limit2).

Methods embodying principles of the present invention make it possible to operate firing plants close to the lean extinction limit and, as a result, to significantly lower the NO_(x) emissions. At the same time, however, the operating characteristic of the burner group staging ratio (BGV_(Rich)) is operated with a certain safety margin to the lean extinction limit so that a stable operation of the burners is ensured. This safety margin, however, is significantly reduced by the described closed-loop control concept.

List of designations 1 Measuring device 2 Filter device 3 Monitoring device 4 Evaluating and control unit BGV_(Rich) Burner group staging ratio, operating characteristic BGV_(New) Burner group staging ratio after adaptation ΔBGV Burner group staging ratio, correction value K_(Filter) Amplification factor used by the filter device 2 K_(PI) Amplification factor used by the evaluating/control unit 4 T_(Filter) Time constant used by the filter device 2 T_(PI) Time constant used by the evaluating/control unit 4 Puls_(Limit) Pulsation limiting value Puls_(Limit1) Upper pulsation limiting value Puls_(Limit2) Lower pulsation limiting value Puls_(Actual) Pressure pulsations measured in the combustion chamber Puls_(Ref) Established pulsation reference value Puls_(Actual, Filter) Pressure pulsations measured and then filtered in the combustion chamber Puls_(Ref, adapt) Adapted or corrected pulsation reference value

While the invention has been described in detail with reference to exemplary embodiments thereof, it will be apparent to one skilled in the art that various changes can be made, and equivalents employed, without departing from the scope of the invention. The foregoing description of the preferred embodiments of the invention has been presented for purposes of illustration and description. It is not intended to be exhaustive or to limit the invention to the precise form disclosed, and modifications and variations are possible in light of the above teachings or may be acquired from practice of the invention. The embodiments were chosen and described in order to explain the principles of the invention and its practical application to enable one skilled in the art to utilize the invention in various embodiments as are suited to the particular use contemplated. It is intended that the scope of the invention be defined by the claims appended hereto, and their equivalents. The entirety of each of the aforementioned documents is incorporated by reference herein. 

1. A method for operating a firing plant having at least one combustion chamber and at least one burner, the firing plant for producing hot gas, the method comprising: defining an operating characteristic for operating the combustion chamber close to the lean extinction limit, in the form of a burner group staging ratio (BGV_(Rich)); measuring, in the combustion chamber, pressure pulsations (Puls_(Actual)(t)); converting said measured pressure pulsations (Puls_(Actual)(t)) into corresponding signals; monitoring exceeding or falling short of at least one pulsation limiting value (Puls_(Limit)); adapting a pulsation reference value (Puls_(Ref)) in dependence upon said monitoring to form an adapted pulsation reference value (Puls_(Ref,adapt)); processing said corresponding signals by a filter device to produce processed pressure pulsations (Puls_(Actual,Filter)(t)); comparing the processed pressure pulsations (Puls_(Actual,Filter)(t)) to the adapted pulsation reference value (Puls_(Ref,adapt)); determining a correction value (ΔBGV) from said comparing; and correcting the burner group staging ratio (BGV_(Rich)) based on said correction value (ΔBGV).
 2. The method as claimed in claim 1, wherein said determining the correction value (ΔBGV) further comprises determining in dependence upon at least one amplification factor (K_(PI)), upon at least one time constant (T_(PI)), or upon both; or the pulsation reference value (Puls_(Ref)), or the amplification factor (K_(PI)), or the time constant (T_(PI)), or combinations thereof, is dependent upon load; or different amplification factors (K_(PI)) and/or time constants (T_(PI)) are taken into consideration for constant load cases and for transient load cases; or combinations thereof.
 3. The method as claimed in claim 2, further comprising: determining different amplification factors (K_(PI)), or time constants (T_(PI)), or both, for constant load cases and for transient load cases.
 4. The method as claimed in claim 1, further comprising: establishing a load-dependent pulsation reference value (Puls_(Ref)); and decreasing or increasing, by a predetermined quantity, the load-dependent pulsation reference value (Puls_(Ref)) when a predetermined number of pulsation values lie above or below the predetermined pulsation limiting value (Puls_(Limit)) within a predefined time period.
 5. The method as claimed in claim 1, comprising performing said method in a closed-loop control circuit.
 6. The method as claimed in claim 1, wherein the firing plant comprises a gas turbine.
 7. The method as claimed in claim 6, wherein the gas turbine comprises a turbine of a power generating plant.
 8. A firing plant comprising: at least one combustion chamber; at least one burner for producing hot gas; wherein a burner group staging ratio (BGV_(Rich)) is defined for operating the combustion chamber close to the lean extinction limit; a measuring device configured and arranged to measure pressure pulsations (Puls_(Actual)(t)) in the combustion chamber; a monitoring device configured and arranged to monitor the level of at least one pulsation limiting value (Puls_(Limit)), to adapt a pulsation reference value (Puls_(Ref)) in dependence upon the level to form an adapted pulsation reference value (Puls_(Ref,adapt)), and to generate at least one signal corresponding to the measured pressure pulsations (Puls_(Ref)(t)); a filter device configured and arranged to process the at least one signal corresponding to the measured pressure pulsations (Puls_(Ref)(t)) and generate processed pressure pulsations (Puls_(Actual,Filter)(t)); and a control unit configured and arranged to compare the processed pressure pulsations (Puls_(Actual,Filter)(t)) with the adapted pulsation reference value (Puls_(Ref,adapt)) and determine a correction value (ΔBGV) by which the burner group staging ratio (BGV_(Rich)) can be corrected.
 9. The device as claimed in claim 8, wherein the filter device comprises a first order filter.
 10. The device as claimed in claim 8, wherein the monitoring device is further configured and arranged change the pulsation reference value (Puls_(Ref)) by a predetermined quantity when, within a defined time period, a predetermined number of pulsation values are outside the at least one pulsation limiting value (Puls_(Limit)).
 11. The device as claimed in claim 8, wherein the control unit comprises a proportional/integral controller, a proportional controller, or an integral controller.
 12. A gas turbine comprising a firing plant as claimed in claim
 8. 13. A power generating plant comprising a gas turbine according to claim
 12. 